Use of silicon-containing particles for protection of industrial materials from UV radiation
a technology of industrial materials and silicon, applied in the direction of silicon compounds, powder paints, coatings, etc., can solve the problems of limiting the lifetime, extremely troublesome, and particularly adverse effects of crystal contamination, and achieve excellent uv protection properties and high optical density
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[0138]FIG. 1a shows a TEM image of the inventive silicon-containing particles.
[0139]FIG. 1b shows the UV-vis spectra of the inventive product 6 (P6) as compared with a typical comparative product TiO2 type P25 (no. 5 in FIG. 1b) from Evonik. Table 1 below discloses, by way of example, the measured absorption (absorption: A, rel. unit) as a function of wavelength (λ [nm]) and as a function of the particle size of samples no. 1 to 5. The arrow points in the direction of increasing median particle size.
TABLE 1UV / vis to IR spectra (FIG. 1b):Spectrum sample no.14352[λ [nm]1.72.42.62.61.62002.711.41.072.32502.311.31.052.13002.711.251.052.13502.31.0310.91.54001.41.020.60.80.84500.750.970.40.720.555000.570.920.30.650.385500.50.880.240.60.266000.350.840.20.560.226500.30.80.160.530.187000.250.790.120.50.147500.220.760.10.480.128000.220.730.10.450.128500.210.670.090.420.119000.180.680.080.40.19500.160.660.060.390.110000.140.650.050.380.11050
[0140]The spectra 1, 2, 3, 4 and 5 of the samples sho...
working example 1
[0157]Obtaining amorphous silicon particles in high-purity form in a free-space reactor. Monosilane is decomposed in an H2 matrix (60% by volume). The hydrogen is used as heat transferer and as diluent gas. The residence time is from 100 to 500 milliseconds in a tubular reactor having a length of 50 cm.
[0158]The cooling and removal of the amorphous silicon is effected in a fluid. In the present case, the decomposition products were passed through liquid paraffin. The amorphous silicon primary particles formed can be stabilized in the paraffin and, according to the production conditions and concentration, are in the form of aggregated primary particles in clusters.
[0159]The particles have different primary particle sizes according to the specific process conditions. The process conditions were:
[0160](a) use of a gas mixture of[0161]2 standard liters (l (STP) / min) of argon, 1 l (STP) / min of argon with 5% by weight of SiH4 for production of samples 3a and 3b.[0162]For sample 3a a resid...
working examples 2a and 2b
[0169](2a) Monosilane was converted in an argon plasma present in a non-thermal equilibrium. The resultant median primary particle size was 5 to 10 nm. The resultant reaction product was dispersed in dilute chloroform. A TEM image of this dispersion is shown in FIG. 8a.
[0170](2b) As experiment (2a), but with extended contact times. Median primary particle sizes of around 30 nm were obtained. The TEM image of the dispersion in dilute chloroform is shown in FIG. 8b.
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